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The results of ultrafiltration tests carried out with model BSA and myoglobin solutions using ceramic 50 and 150 kDa membranes have been presented. Membrane permeability and selectivity were investigated in function of pH, transmembrane pressure (TMP) as well as molecular modelling data for proteins such as size, geometrical parameters and pH of minimal free energy of folding. The study has shown that the permeate flux J(v) depends on TMP, whereas the protein rejection is mainly influenced by pH. The results demonstrated that molecular modelling data are not sufficient to explain the membrane behaviour and the membrane–protein charge interactions and fouling effects must be also considered to explain the rejection mechanisms.
Czasopismo
Rocznik
Tom
Strony
135--141
Opis fizyczny
Bibliogr. 15 poz., rys.
Twórcy
autor
- Transport Engineering and Economics Faculty, Maritime University of Szczecin, ul. Henryka Pobożnego 11, 70-507 Szczecin, Poland
autor
- Transport Engineering and Economics Faculty, Maritime University of Szczecin, ul. Henryka Pobożnego 11, 70-507 Szczecin, Poland
autor
- Marine Engineering Faculty, Maritime University of Szczecin, Wały Chrobrego 1–2, 70-500 Szczecin, Poland
Bibliografia
- [1] ALFONSO M.D., BORGUES R., Review of the treatment of seafood processing wastewaters and recovery therein by membrane separation processes. Prospect of ultrafiltration of wastewaters from the fish meal industry, Desalination, 2002, 142, 29.
- [2] HUANG L., MORRISSEY M.T., Fouling of membranes during microfiltration of surimi wash water. Roles of pore blocking and surface cake formation, J. Membrane Sci., 1998, 144, 113.
- [3] SRIDANG P.C., KAIMAN J., POTTIER A., WISNIEWSKI C., Benefits of MBR in seafood wastewater treatment and water reuse, Desalination, 2006, 200, 712.
- [4] AFONSO M.D., BÓRQUEZ R., Nanofiltration of wastewaters from fish meal industry, Desalination, 2002, 151, 131.
- [5] CASANI S., LETH T., KNØCHEL S., Water reuse in a shrimp processing line. Safety considerations using a HACCP approach, Food Control, 2006, 17, 540.
- [6] CASA E.J., GUADIX A., IBANEZ I., GUADIX E.M., Influence of pH and salt concentration on cross-flow microfiltration of BSA through ceramic membranes, Biochem. Eng. J., 2007, 33, 110.
- [7] NOORDMAN T.R., KETELAAR T.H., DONKERS F., WESSELINGH J.A., Concentration and desalination of protein solutions by ultrafiltration, Chem. Eng. Sci., 2002, 57, 693.
- [8] KUCA M., SZANIAWSKA D., Application of microfiltration and ceramic membranes for treatment of salted aqueous effluents from fish processing, Desalination, 2009, 241, 227.
- [9] KUCA M., Application of ultrafiltration for regeneration of waste brine from fish processing, Thesis, West Pomeranian University of Technology, Szczecin 2009 (in Polish).
- [10] Food Chemistry. Saccharides, Lipids and Proteins, Z.E. Sikorski (Ed.), Vol. 2, Wydawnictwa Naukowo- Techniczne WNT, Warsaw 2007 (in Polish).
- [11] PEDRETTI A., VILLA L., VISTOLI G., Vega. A versatile program to convert, handle and visualize molecular structure on Windows-based PCs, J. Mol. Graph., 2002, 21, 47.
- [12] LI H., ROBERTSON A.D., JENSEN J.H., Very fast empirical prediction and rationalization of protein pKa values, Proteins: Structure, Function, and Bioinformatics, 2005, 61, 704.
- [13] KISSICK D.J., DETTMAR C.M., BECKER M., MULICHAK A.M., CHEREZOV V., GINELL S.L., BATTAILE K.P., KEEFE L.J., FISCHETTI R.F., SIMPSON G.J., Towards protein-crystal centering using second-harmonic generation (SHG) microscopy, Acta Crystallogr., 2013, Sect. D, 69, 843.
- [14] BUJACZ A., Structures of bovine, equine and leporine serum albumin, Acta Crystallogr., 2012, Sect. D, 68, 1278.
- [15] PETTERSEN E.F., GODDARD T.D., HUANG C.C., COUCH G.S., GREENBLATT D.M., MENG E.C., FERRIN T.E., UCSF Chimera. A visualization system for exploratory research and analysis, J. Comput. Chem., 2004, 25 (13), 1605
Typ dokumentu
Bibliografia
Identyfikator YADDA
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